• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The present invention is a group of new polymers and treated, semi-permeable, polymeric membranes made from the new polymers, having improved selectivity for separating components of a gas mixture. The membrane is provided by fluorinating a polymer cast into membrane form, having the general structural formula: Wherein R₁ is H or a C₁-C₂ alkyl group; R₂ and R₃ are independently linear or branched C₁-C₆ alkyl groups; R₄ is a linear or branched C₁-C₁₂ alkyl or aryl group; X is a C₁-C₃ alkyl group or phenyl; m is at least 100; and n is 0 or 1.
    公开号:SU1741609A3
    申请号:SU874203870
    申请日:1987-12-07
    公开日:1992-06-15
    发明作者:Лангзам Майкл；Коутс Лешер Савока Энн
    申请人:Эр Продактс Энд Кемикалз Инк (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to polymeric membranes used to separate gas mixtures, and can be used in chemical technology and chromatography processes.
    The purpose of the invention is to increase the selectivity of the separation of gases,
    PRI me R 1 „Synthesis of political polymethylmilpropine (PTMPP).
    In a one-liter three-neck vessel equipped with a mechanical stirrer, a pressure equalizing funnel, and a tube for supplying gas with a finger cooler, methyl lithium (0.13 l of a 1.6 M solution in diethyl ether) and 0.225 l of anhydrous
    diethyl ether under a nitrogen atmosphere. The vessel is cooled to 30et and the refrigerator is filled with dry ice and isopropanol. Then, propyne is introduced through a gas supply tube, which results in the formation of a white, viscous slime. The reaction mixture is allowed to warm to room temperature for 2 hours and then cooled again to 0 ° C, after which trimethylgermanium chloride (2.8 g, 0.162 mol) is added dropwise to it within 10 minutes. After further stirring for 2 hours at room temperature, the mixture of products is diluted with pentane and washed with distilled water.
    -H
    ABOUT
    Yu
    water to remove lithium salts. The organic layer is dried over anhydrous magnesium sulphate, the drying agent is filtered off and, in the concentrator, pentane is distilled off. As a result of the distillation of the obtained product at atmospheric pressure, about using a column packed with glass spirals, a column of 15 mm in size, half a mile and trimethylgermylpropin (b.p. 109 - 1124).
    100 g of toluene is mixed with a catalyst with a pentachloride and the mixture is stirred for about 5 minutes to obtain a solution of light yellow color. Approximately 19 g of tri-methylgermpropin (TMGP) is added to the solution, after which it immediately becomes dark brown. Within a few seconds, a noticeable increase in the viscosity of the solution occurs. After 2k hours, the reaction mixture is treated with methanol, washed with 1000 ml of methanol and then dried. The result is a polymer - polytetramethyl-hermylpropin (PTMP) with the following structure
    nosti. Smooth sheet membranes are mounted in a CSC-135 cell to determine permeability.
    Some of the membranes, not yet removed from the glass substrate, are treated with fluorine in a gas-phase mixing-type reactor with various fluorine / nitrogen mixtures. Membranes will interfere in
    The reactor and gas volume are flushed with nitrogen for k hours to remove ambient air. A mixture of predetermined ratios VNfc is then passed through the reactor for 5 times before the predetermined time.
    Some polymer membranes are fluorinated according to the above procedure using various concentrations of fluorine in the gas mixture. A study of the surface composition of the membranes after fluorination reveals significant changes in the surface of the membranes. The composition of the surface of fluorinated membranes and two non-fluorinated PTMGP membranes was investigated, the results are given below in Table 1.
    CHi
    --OS-7,
    I j
    100
    H3C-Ge-CH3
    CH3,

    By varying the ratio of monomer and catalyst — pichloride tali, the molecular weight of the polymer can be controlled. The polymer obtained is soluble in carbon disulfide and insoluble in chloroform and toluene.
    A polymeric membrane in the form of a smooth sheet is prepared from a solution of polymer in carbon disulfide, taken at a weight ratio. The polymer concentration in the solution is 2.5% by weight.
    A portion of the polymer solution in carbon disulfide with a 1 mm knife is poured onto a clean, smooth glass surface and air dried using a stream of dry nitrogen. The film thickness fluctuates around 25 75 microns. The smooth sheet membranes are removed from the solid glass substrate by immersing the latter in water. Films are easily removed from the glass surface.
    0
    five
    S
    O
    five
    The surface analysis data presented in Table 1 indicates a significant drop in the content of both carbon and germanium on the surface of fluorinated membranes. The oxygen concentration shown in the control samples is water adsorbed on the surface of the polymer.
    Data on the gas permeability and selectivity of polymer membranes treated with gas mixtures with different concentrations of fluorine and at different contact times are given in the following examples.
    EXAMPLE 2: One non-fluorinated and one fluorinated smooth sheet membrane sample made in the described manner, install p CSC cells to determine the permeability of each individual cell so that the pressurized gas mixture can pass through the membrane surface and the passed gas flow can be measured on the other side of the membrane with an instrument for measuring the volumetric flow.
    Permeability (P), specific permeability (P) L, selectivity (Oi) of various gases through the membranes are given in Tables 2 and 3, respectively.
    For both membranes, time .90s CM3 / Ng / MHH100 cmu / РЈ / min1 F,% 1 Р2 / смЗ (total) 15
    The results shown in Tables 2 and 3 indicate a significant increase in selectivity for membranes subjected to fluoridation with respect to all six gas mixtures selected for testing.
    Example The membranes of example 1 are treated with fluorine (100 F pulses). As a control option, use the same membrane without treatment.
    In accordance with the procedure given in Example 1, the permeability, specific permeability and selectivity of the membranes for different gases are determined.
    The polymer structures of the membranes subjected to testing and the results of the determination of gas permeability are given in Tables A and 5 below.
    From the data table. and 5, fluorine treatment increases the selectivity of membranes that contain methyl or ethyl groups bound to a germanium atom, to a significant extent. With increasing alkyl, the effect of fluorination decreases.
    Example The same polymerization and membrane synthesis technique as in Example 1 is used to produce membranes having a polymeric structure comprising TMGP and trimethylsilylpropyn (Tmep) units.
    Table 6 shows the polymerization times for various combinations of copolymers.
    to
     As can be seen from the data of Table 6, the presence of even a small amount of TMPP significantly accelerates the polymerization. This rapid polymerization allows the synthesis of thin polymer films to be carried out, which is extremely difficult in the case when only TMPP monomers are used.
    Polytrimethylsilypropinic, re. Litrimethylgermylpropane membranes
    ,

    1609
    and two membranes made from polymer obtained by joint polymerization of TMSP and TMIP monomers were not treated with fluorine according to the procedure described above. Permeability and selectivity with respect to different gases and gas mixtures were determined for fluorinated membranes (like for untreated membranes, control).
    Below are the results of these studies in table 7 and 8.
    PRI me R 5 (control). The fluorination technique described above is used to process silicone rubber and poly-2-nonin polymers.
    Silicone rubber, which is a cross-linked polymer having the general structural formula
    15
    20
    sn3 --si-o-I
    - CH3J
    obtained in the form of a membrane, quite
    permeable to various gases, but exhibits relatively low selectivity, a commercial silicone rubber membrane (MEM-100, B-163 batch manufactured by General Electric) with a thickness of 0.127 mm is fluorinated with a gas stream containing 0.5% rasa, 5 min Permeability and self-diffusivity with respect to different gayai @ & shi are measured for both fluorinated and non-fluorinated membranes. Gas permeability values and membrane surface analysis results for fluorinated and non-fluorinated membranes
    are given in tab. 9o
    Poly-2-nonin is formed into a dense membrane and subjected to Fa / N-z treatment for 15 minutes. gas stream containing 0.5% F., gas. Samples of fluorinated and non-fluorinated membranes are examined to determine the permeability and selectivity with respect to different gases, the analysis data are given in Table 10.
    Poly-α-nonine membranes after-treatment with a reactive mixture have a highly fluorinated surface, but this treatment does not lead to significant 17 M609
    no change in permeability,
    nor selectivity with respect to the gas mixtures studied.
    eight
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    I - I
    Rf-ge-rj l
    The method of producing a polymeric membrane. I. K2
    wounds for the separation of gas mixtures where R, kЈG R represent CH by casting metal-containing poly- or
      h or its copolymer with trimethylsilynpropine at a molar ratio of germanium and silyl-containing units of 2 to 90: 10 98, respectively, and the polymer film is treated with gas-propene as a film, followed by treatment with gaseous fluorine, characterized in Germanium-containing polypropin with a structural formula is used as a metal-containing polypropin.
    15
    a different mixture of fluorine and nitrogen at a concentration of fluorine in a mixture of 1 rd for 90 - 750 s.
    eight
    - I
    propyne at a molar ratio of germanium and silyl-containing units of 2–90: 10 98, respectively, and the polymer film is treated with gas
    a different mixture of fluorine and nitrogen at a concentration of fluorine in a mixture of 1 rd for 90 - 750 s.
    Table 1
    Note: (
    (2) selectivity determined by the permeability coefficient (P) of the composite membrane;
    (3) selectivity determined by (P / 1) fluorinated surface „
    1741609
    ten
    Continuation of table 2
    (2) permeability coefficient for composite membrane membrane Yu + 10.
    ablit
    R4 RteRteCH3
    R, -Ra-v uH5
    R5-C4H9
    Note: (1) 100 pulses;
    (2) permeability coefficient of the composite membrane ().
    (3) conductivity of the fluorinated surface layer
    (NO4).
    TableZK, Ke «1C CH3R {RZ R y CtUsR C4Hg
    Note: (1) 100 pulses;
    (2) selectivity determined by the permeability coefficient (P) of the composite membrane;
    (3) selectivity, determined by the conductivity CP / L) of the fluorinated surface layer.
    Table
    Note: (1) 125 F2 pulses.
    - (2) NTO pulses F2.
    (3) The permeability coefficient of the composite membrane (K10 + | c).
    CO Conductivity of the fluorinated surface layer (MO49).
    Table 6
    15
     Note: (1) 125 F pulses.
    (2) 100 Fg pulses.
    (3) Selectivity, determined by the permeability coefficient / P / composite membrane.
    () Selectivity determined by the conductivity of the /P/L/fluorinated surface layer.
    Table}
    Gas
    Non-fluorinated fluorinated
    Helium
    Oxygen
    Nitrogen Methane
    16 Tables
    Membranes
    291
    1bz 523
    Table 10
    Data analysis of the surface method BBSD, g
    C o
    1741609
    18 Continuation of the table.
    43.7 46.2 49.8
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    引用文献:
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